Method and system for treating polluted water

Abstract: An oxidizing agent is added to water polluted with organic compounds, especially organic chlorine compounds, disinfection is carried out, and suspended solids in the water are removed. Thereafter, ultraviolet rays are irradiated to oxidize and decompose the organic compounds, and furthermore volatile organic compounds are separated and removed from the water. Finally, the oxidizing agents remaining in the water are reduced. The oxidizing agent is separately added at two phases of disinfection and oxidization decomposition, thereby causing the decomposing efficiency of organic compounds to be much improved.

Description: The present invention relates to a method and system for treating water polluted with organic compounds such as organic chlorine compounds. Recently, rivers, lakes, ponds and groundwater have been contaminated with harmful substances. In the case where the river, lake, pond or groundwater is intended to be used for drinking water and/or industrial water, it will not be usable as it is. Public attention has been given to this great social problem. It has been said that almost all contamination of rivers and groundwater are caused by industrial and living waste water having flowed thereinto. It has been pointed out that the treatment and control of organic compounds, such as organic chlorine compounds, etc, for example trichloroethylene, etc. flowed out from various kinds of factories and dry cleaning plants in the past were insufficient. Conventionally, as treating technologies of trichloroethylene, etc. in waste solutions, an activated carbon adsorption method, another adsorption method such as high molecular adsorption, reduction by metal iron are already known. The activated carbon adsorption method has been widely utilized at present. However, there are many cases where a great deal of dissoluble iron, manganese, silica, suspended solids, organic substances, such as humic acid, are contained in water containing trichloroethylene or organic compounds, such as agricultural chemicals. There is a problem that activated carbon is saturated with the above substances, thereby causing effective treatment of the organic chlorine compounds to be spoiled. To solve this problem, an ultraviolet rays degradation treatment method was developed, wherein oxidative decomposition of organic chlorine compounds is made by irradiating ultraviolet rays in consideration with oxidizing agents, such as ozone (see US-A-5234606). However, with this method, although it is possible to decompose organic chlorine compounds, such as trichloroethylene, tetrachloroethylene, 1,1,1-trichloroethane, chloroform, etc, there is a great difference in the quantity of ultraviolet irradiation required to decompose different types of substances treated. According to experiments, for example the quantity of ultraviolet irradiation necessary to decrease the initial concentration of 0.5mg/ℓ of 1,1,1-trichloroethane to 0.001mg/ℓ is 100 or more in the case that the quantity thereof for trichloroethylene is 1. In the case where the organic chlorine compounds require a large quantity of ultraviolet irradiation to decompose, an ultraviolet rays destruction treatment method as disclosed in US-A-5234606 will need a large-scale system. On the other hand, for example, in the case where the quantity of hydrogen peroxide to be added is little, the reaction for decomposition is slow, and in the case where the concentration of organic substances other than organic chlorine compounds is high, the organic substances consume the hydrogen peroxide earlier than the organic chlorine compounds do. Therefore, it is hard to decompose the organic chlorine compounds. In the case where hydrogen peroxide is excessively supplied, the ultraviolet rays will be absorbed in hydrogen peroxide, and added hydrogen peroxide will not be sufficiently decomposed. As a result, organic chlorine compounds are not decomposed. Furthermore, in the case where a gas, such as ozone, is utilized as an oxidizing agent, the decomposition by ultraviolet rays with ozone will hardly proceed if only ozone is added, at the beginning of the treatment, to the water to be treated. Attention is also drawn to the disclosures of US-A-5180499 and WO-A-93/25297. It is an object of the present invention to provide a method for completely treating organic compounds, such as organic chlorine compounds, in water to be treated (hereinafter called "waste water" or "polluted water"), by treating the waste water with ultraviolet light after an oxidizing agent is separately added to the waste water both in the disinfection process of the waste water and just before the decomposition process of organic compounds in the water polluted and contaminated with trichloroethylene, 1,1,1-trichloroethane etc. It is another object of the invention to provide a method for treating organic chlorine compounds remaining in the waste water after decomposition treatment together with adsorption treatment utilizing gas-water contact and activated carbon. It is a further object of the invention to provide a method which increases the treatment efficiency by suppressing the generation of bacteria in tanks and piping by the addition of oxidizing agents to the waste water, removing minute suspended solids in the waste water through filtration, and reducing the oxidizing agents which may slightly remain even after the ultraviolet rays decomposition, and which can adjust and/or control the changes of pH in water due to chlorine ions generated by the decomposition of organic chlorine compounds, etc. It is a still further object of the invention to provide a system comprising at least a disinfection unit, a decomposition unit and an oxidizing agent supplying unit, which completely decompose organic compounds such as organic chlorine compounds in waste water with ultraviolet rays after an oxidizing agent is added to the waste water through the oxidizing agent supplying unit at the time of disinfection of the waste water by the disinfection unit and just before the decomposition of organic compounds in the decomposition unit. The present invention in one aspect provides a method of treating waste water containing organic compounds, comprising: adding a first amount of an oxidizing agent into said waste water to disinfect bacteria contained in said waste water, said first amount being suitable to substantially disinfect the bacteria contained in the waste water; removing solid material contained in said waste water treated with said oxidizing agent; adding a second amount of said oxidizing agent into said treated waste water, said second amount being selected such that the second amount and a part of the first amount remaining in the waste water are suitable to form hydroxy radicals for sufficiently decomposing the organic compounds in the waste water when ultraviolet rays are irradiated; irradiating the ultraviolet rays onto said treated waste water containing said oxidizing agent to form the active hydroxy radicals so that the organic compounds are decomposed by the hydroxy radicals formed by the part of the first amount and the second amount of the oxidizing agent; and removing said oxidizing agents remaining in said treated waste water. The method according to the invention preferably additionally comprises the further step of exposing forcibly the waste water to air so that volatile organic materials contained in the waste water are retained in the air to adsorb onto activated carbon, subsequent to said decomposition step by irradiating with ultraviolet rays. The invention in another aspect provides a system for treating waste water containing organic compounds, comprising: a disinfection unit for disinfecting bacteria contained in the waste water; a suspended solid removing device for separating solid substance contained in the waste water treated by the disinfection unit; a decomposition unit having an ultraviolet ray lamp therein, said decomposition unit decomposing by the ultraviolet ray lamp the organic compounds contained in the waste water after suspended solid is removed; an oxidizing agent supplying unit for supplying an oxidizing agent to the disinfection unit and the decomposition unit, said oxidizing agent disinfecting the bacteria contained in the waste water when supplied at the disinfection unit and forming hydroxy radicals when irradiated by the ultraviolet rays to decompose the organic compounds at the decomposition unit; and an oxidizing agent removing unit for eliminating the oxidizing agent remaining in the waste water treated at the decomposition unit, said oxidizing agent removing unit including at least one of reducing agent, activated carbon and catalyst to remove the oxidizing agent in the waste water. The system for treating waste water according to the invention preferably further comprises a gas-liquid contact/adsorption unit for forcibly exposing the waste water to air after the organic compounds are decomposed, volatile organic material contained in the waste water being retained in said air and being adsorbed onto activated carbon, wherein said gas-liquid contact/adsorption unit includes an air-exposing tank for receiving the waste water from the decomposition unit, air being fed into the waste water to catch the volatile organic materials in the air to separate from liquid, and an activated carbon layer having activated carbon, said activated carbon layer absorbing the volatile organic material in the air. The method according to a preferred aspect of the invention will be described with reference to the processes thereof, which are divided into first to fifth processes. The first to fifth processes merely show a primary sequence. Therefore, supplementary processes or treatment may be provided between the processes and/or the sequential order of some processes may be changed. The first process of the invention is a disinfection process where bacteria contained in waste water (polluted water), such as contaminated groundwater, is disinfected. Therefore, no bacteria is generated in the pipings, filters, various valves, flow meters, level meters, etc., which are located downstream of the disinfection process. The disinfection is carried out by adding oxidizing agents to the waste water. Hydrogen peroxide, sodium hypochlorite, hydrochloric acid, etc. or ozone is used as an oxidizing agent to be added to the waste water. It is preferable that sodium hypochlorite and hydrochloric acid are not used because there is a possibility to generate a secondary pollution since they have chloric ions. Ozone is a gas and is less dissolved into water. However, as it is easy to make gas-liquid contact by using a static mixer, ozone is effective. However, hydrogen peroxide is most preferable because it is very easy to handle. The second process is for removing solid material (suspended solids) contained in the waste water. Namely, suspended solids in the waste water are removed by using a filter or by agglomeration and sedimentation therof. An adequate amount of oxidizing agent is supplied in the first disinfection process and just before the decomposition treatment of the third process. For example, hydrogen peroxide is used for disinfection in the disinfection process, and the residual oxidizing agent carried over in the waste water is also used in the decomposition treatment of the third process. As a matter of course, in the third process, it is possible to decompose organic matters by adding the oxidizing agent to the waste water just before the decomposition treatment of the third process. The third process is a decomposition treatment for organic compounds, where organic compounds, such as organic chlorine compounds, are decomposed by irradiating with ultraviolet rays to the waste water containing the residual oxidizing agent, which has passed through the second process, and oxidizing agent which is newly added just before the third process. In the third decomposition process, where the amount of oxidizing agent, such as hydrogen peroxide, ozone, etc. is to little or too much, it is hard to complete the decomposition. This is because hydrogen peroxide, ozone, etc. absorb ultraviolet rays. Hydrogen peroxide, ozone, etc absorb ultraviolet rays and then generate active hydroxy radicals (·OH), which contribute to the decomposition of the organic matter. However, where there is an excessive amount of oxidizing agent, the ultraviolet rays are absorbed by the oxidizing agent to cause the oxidizing agent located in the vicinity of ultraviolet rays to be decomposed. Therefore, the entire amount of oxidizing agent in the water is not effectively decomposed. The amount of hydrogen peroxide before the third process is lessened and hydrogen peroxide is newly added in the third process, thereby causing reliable decomposing conditions to be established. As ultraviolet rays are irradiated to the polluted water containing the oxidizing agent, active hydroxy radicals are generated in the polluted water, and the said radicals decompose the organic compounds, etc. Furthermore, a cylinder type or vessel type may be permitted to be used for the ultraviolet rays decomposing unit. However, the cylinder type is more preferable and advantageous from the standpoints of installation space, maintenability and effective irradiation of ultraviolet rays. Still furthermore, either one of a high pressure mercury lamp, medium pressure mercury lamp or low pressure mercury lamp may be used as an ultraviolet rays lamp. However, in the case where hydrogen peroxide or ozone is used as an oxidizing agent, it is preferable that a low pressure mercury lamp or a medium pressure mercury lamp, which has a great deal of energy at the wave length of 253.7 nm be used to efficiently decompose hydrogen peroxide or ozone. The fourth process is a gas-liquid contact and adsorption treatment, where air is blown into the polluted water for aeration in order to cause gas-liquid contact between the volatile non-decomposed substances carried over in the waste water and air to be carried out. Accordingly, volatile organic matters such as organic chlorine compounds, etc., in the waste water are transferred from liquid phase to gaseous phase. Thereafter, they are adsorbed with activated carbon. The fifth process is a residual oxidizing agent removing treatment, where the oxidizing agents carried over in the waste water are treated and removed using a reducing agent, activated carbon, catalyst resin, etc. In the case where the organic compounds contained in the waste water are substances that may be comparatively easily decomposed, such as trichloroethylene, tetrachloroethylene, dichloroethylene, etc., the substances can be removed from the water utilizing only the residual oxidizing agent removing process. Therefore, it is possible to omit the gas-liquid contact and adsorption treatment process. As described above, for the purpose of explanation, the gas-liquid contact and adsorption treatment is regarded as the fourth process, and the residual oxidizing agent removing treatment is regarded as the fifth process. However, either one of the gas-liquid contact and adsorption treatment or the residual oxidizing agent removing treatment may precede the other. In the third process, as organic compounds such as organic chlorine compounds, etc., are decomposed by oxidation, chlorine may be generated, and especially in the case where the concentration of the organic chlorine compounds is high, the pH thereof will be remarkably lowered. In this case, alkali agents are added in the third process to adjust pH thereof in order to carry out oxidization decomposition, or alkali agents are added between the decomposition treatment and the residual oxidizing agents removing treatment to adjust pH thereof. Any one of potassium hydroxide, sodium hydroxide, calcium hydroxide, sodium carbonate, etc may be used as an alkali agent. However, the alkali agent that is most preferably used for the treatment is sodium hydroxide. In the treatment method according to the invention, it is easier and more efficient to treat organic compounds than with the conventional method even in cases where two or more kinds of organic compounds, such as organic chlorine compounds, exist in the waste water and where organic compounds, such as organic chlorine compounds, which need a larger quantity of ultraviolet irradiation to decompose the constituents are included. Also, by adding the oxidizing agents to the waste water in a more favourable state, the decomposition efficiency can be increased. Therefore, in the treatment method according to the invention, water polluted with organic compounds is removed when it is used for treating groundwater, rivers, waste water discharged from factories and cleaning plants. The invention will be further described, by way of example only, with reference to the accompanying drawings, in which: Fig. 1 is a diagrammatic view showing a preferred embodiment of a waste water treating system of the invention; Fig. 2 is a graph showing a comparison of the decomposition effects of trichloroethylene when an oxidizing agent is added to the Test Water through one point and when the oxidizing agent is added to the Test Water through two points, both using the Test Water 1 and Test Water 2; Fig. 3 is a graph showing a comparison of the decomposition effects of 1,1,1-trichloroethane when an oxidizing agent is added to the Test Water through one point and when the oxidizing agent is added to the Test Water through two points, both using the Test Water 1 and Test Water 3; Fig. 4 is a graph showing a comparison of the decomposition effects of trichloroethylene when an oxidizing agent is added to the Test Water through one point and when the oxidizing agent is added to the Test Water through two points, both using the Test Water 1 and Test Water 2; Fig. 5 is a graph showing a comparison of the decomposition effects of 1,1,1-trichloroethane when an oxidizing agent is added to the Test Water through one point and when the oxidizing agent is added to the Test Water through two points, both using the Test Water 1 and Test Water 3; Fig. 6 is a graph for the Test Water 1, showing another comparison of the decomposition effects of trichloroethylene and 1,1,1-trichloroethane when the oxidizing agent is added to the Test Water through one point and two points; Fig. 7 is a graph showing the effects of removal in the aeration of the Test Water 1 that is the waste water containing 1,1,1-trichloroethane; Fig. 8 is a graph showing a comparison of the decomposition effects of trichloroethylene when an oxidizing agent is added to the Test Water through one point and when the oxidizing agent is added to the Test Water through two points, both using the Test Water 1 and Test Water 2; Fig. 9 is a diagrammatic view showing a preferred embodiment of a gas-liquid contact and adsorption unit; Fig. 10 is a diagrammatic view showing another preferred embodiment of the invention; and Fig. 11 is a diagrammatic view showing still another preferred embodiment of the invention. With reference to the accompanying drawings, preferred embodiments of the invention will be described. The preferred embodiments show treatment examples of waste water containing trichloroethylene and 1,1,1-trichloroethane. When treating, a unit shown in Fig. 1 is used. The specification of the unit is shown in Table 1 below: First process Disinfection treatment and oxidizing agents addition 30% hydrogen peroxide, pump Second process Suspended solids removing treatment 10-micron cartridge filter Oxidizing agents added 30%, H 2 O 2 , Pump used. Third process Decomposition treatment Unit capacity: 3.2 liters Unit material: Stainless steel Jacket material: Quartz Lamp type: Low pressure mercury lamp, OGL30W-2 Lamp capacity: 30 watts bulb x three lamps pH adjustment 2% Sodium hydroxide Fourth process Gas-liquid contact and adsorption treatment Aeration type gas-liquid contact unit Activated carbon (fibrous) Fifth process Residual oxidizing agents removing treatment 10% sodium bisulfide The residual oxidizing agents removing treatment may be carried out as the fourth process, and the gas-liquid contact and adsorption treatment may be performed as the fifth process. In Fig. 1, a guaranteed reagent of trichloroethylene and a guaranteed reagent of 1,1,1-trichloroethane were dissolved in a graduated flask in advance, poured into a tank 1 and diluted with pure water to make 40ℓ. At this time, the trichloroethylene concentration ranges from 0.05 to 8mg/ℓ, and the 1,1,1-trichloroethane concentration ranges from 0.05 to 8mg/ℓ. The number of live bacteria was 180 per milliliter. This was used as Test Water. Hereinafter, this Test Water was named Test Water 1. Separately from the Test Water 1, trichloroethylene and 1,1,1-trichloroethane were separately diluted with water to make Test Water, of which the concentration was in a range from 0.05 to 8mg/ℓ, respectively. The Test Water having only trichloroethylene was named Test Water 2, and the Test Water having only 1,1,1-trichloroethane was named Test Water 3. With each of the Test Waters used as water to be treated, the following experiments were carried out. The details of the experiments are as follows; firstly, the Test Water was transferred from the tank 1 by a pump 2, filtrated by a cartridge filter 3 and stored in a tank 4. Hydrogen peroxide was used as an oxidizing agent. The hydrogen peroxide was supplied from a hydrogen peroxide tank 11 into the tank 1 by a pump 12 and was sent into a pipe between a flow meter 6 and a decomposition tank 7 by a pump 17a. The hydrogen peroxide concentration in the tank 4 was set to about 50mg/ℓ. The Test Water 1 with hydrogen peroxide reserved in the tank 4 was sent into the decomposition tank 7 through the flow meter 6 by a pump 5, wherein the trichloroethylene and 1,1,1-trichloroethane are decomposed. Fig. 2 shows the results of the decomposition test conducted on the Test Water containing the trichloroethylene, which refer to the results in the respective cases, one of which is a case where hydrogen peroxide having a concentration of 50mg/ℓ was added only into the tank 1 (disinfection unit), and the other of which is a case where the same hydrogen peroxide was added to the tank 1 and just before the decomposition tank 7. The Test Water 2 in which only trichloroethylene of an initial concentration of 8mg/ℓ is contained and the Test Water 1 in which trichloroethylene and 1,1,1-trichloroethane both having an initial concentration of 8mg/ℓ are simultaneously contained were respectively put in the tank 1 as water to be treated. (1) and (2) in Fig. 2 show the results of the Test Water 2 having only trichloroethylene in the water to be treated. (1) shows the results where hydrogen peroxide was added to only the tank 1, and (2) shows the results where hydrogen peroxide was added to the tank 1 and just before the decomposition unit 7. (3) and (4) show the results of the Test Water 1 which simultaneously contains trichloroethylene and 1,1,1-trichloroethane. (3) shows the results where hydrogen peroxide was added to only the tank 1, and (4) shows the results where hydrogen peroxide was added to the tank 1 and just before the decomposition unit 7. As is clear from the comparison between the results of (1) and (2) and those of (3) and (4), it is easily understandable that separately adding hydrogen peroxide is more effective than a single adding thereof. It is understandable from the comparison between (1) and (3) that, in a case where the trichloroethylene and 1,1,1-trichloroethane are contained at the same time, as the decomposing efficiency is remarkably poor only with the adding of hydrogen peroxide into the tank 1, compared with the case where trichloroethylene is contained alone, almost the same results as the case where trichloroethylene is contained alone can be obtained by adding hydrogen peroxide just before the decomposing unit 7. Judging from the results of (1) and (3), it is apparent that easily decomposed substance (trichloroethylene) is suppressed if other substance (1,1,1-trichloroethane) is contained. Fig. 3 shows the results of the decomposition test conducted on the Test Water 3 containing 1,1,1-trichloroethane, wherein (5) shows a case where hydrogen peroxide was added to only the tank 1, and (6) shows a case where hydrogen peroxide was added to the tank 1 and just before the decomposition unit 7. (7) and (8) show the results for the Test Water 1, wherein (7) shows a case where hydrogen peroxide was added to only the tank 1, and (8) shows a case where hydrogen peroxide was added to the tank 1 and just before the decomposition unit 7. As is clear from a comparison of (5) and (6) or (7) and (8), it is considerably advantageous to decompose organic matters if hydrogen peroxide is separately added. From a comparison between (5) and (7), it is understandable that, in the case where the trichloroethylene and 1,1,1-trichloroethane are contained at the same time, the decomposing ratio is remarkably poor only with the adding of hydrogen peroxide into the tank 1, compared with the case where 1,1,1-trichloroethane alone was contained. However, by further adding hydrogen peroxide just before the decomposing unit 7, it is clear that the decomposing ratio was improved to a considerable extent. For the Test Water 1, 2 and 3, similar experiments were carried out in one case where the hydrogen peroxide adding amount is 300mg/ℓ which is a little excessive. Fig. 4 shows the results of the decomposing effect of trichloroethylene in the water to be treated, and Fig. 5 shows the results of the decomposing effect of 1,1,1-trichloroethane in the water to be treated. In Fig. 4, (9) and (10) are the measured values of the Test Water 2 containing only trichloroethylene in the water to be treated. (9) shows the results where hydrogen peroxide was added to only the tank 1, and (10) shows the results where hydrogen peroxide was added to the tank 1 and just before the decomposing unit 7. (11) and (12) show the results of the Test Water 1 which simultaneously contains trichloroethylene and 1,1,1-trichloroethane in the water to be treated. (11) shows the results where hydrogen peroxide was added to only the tank 1, and (12) shows the results where hydrogen peroxide was added to the tank 1 and just before the decomposing unit 7. Fig. 5 shows the measurement results for Test Water 3. (13) shows the results where hydrogen peroxide was added to only the tank 1, and (14) shows the results where hydrogen peroxide was added to the tank 1 and just before the decomposing unit 7. (15) and (16) are the measured results of the Test Water 1. (15) shows the results where hydrogen peroxide was added to only the tank 1, and (16) shows the results where hydrogen peroxide was added to the tank 1 and just before the decomposing unit 7. The results in the case where the hydrogen peroxide adding amount was 300mg/ℓ are almost the same as the results in the case where it was 50mg/ℓ. It is clear that it is more effective to add hydrogen peroxide separately to the initial stage and just before the decomposing unit than adding it only to the initial stage. Next, as regards the Test Water 1 which simultaneously contains trichloroethylene at 8mg/ℓ and 1,1,1-trichloroethane at 8mg/ℓ, the decomposing experiment was carried out by irradiating ultraviolet rays in such a state that hydrogen peroxide, of which the concentration was 50mg/ℓ, was added to the tank 1 and just before the decomposing unit 7 until the quantity of the ultraviolet irradiation reached 5kwh per cubic meter. The measured results thereof are shown in Fig. 6. (17) shows the fluctuation of the concentration of trichloroethylene and (18) shows the fluctuation of the concentration of 1,1,1-trichloroethane. When the quantity of ultraviolet irradiation was 5kwh per cubic meter, the residual concentration of trichloroethylene was less than 0.001mg/ℓ, which is less than the detectable level. As regards 1,1,1-trchloroethane, the initial concentration thereof was decreased only to 3.1mg/ℓ. The concentration thereof is not permitted to discharge as it is as usual waste water. Therefore, as shown in Figs. 1 and 9, the Test Water was stored in a tank 8 and sent to the gas liquid contact/absorption unit 9. Air was supplied into the tank 8 at an air volume of 100 liters per hour by using an air pump (not illustrated) incorporated in the gas-liquid contact/adsorption unit 9 in order to cause the Test Water 1 to be exposed to air. Then, the concentration of 1,1,1-trichloroethane was measured at five-minute intervals. Fig. 7 shows the results thereof. In five minutes, the concentration became 0.1mg/ℓ, in ten minutes 0.007mg/ℓ, in fifteen minutes 0.003mg/ℓ, in twenty minutes 0.0011mg/ℓ, and in twenty-five minutes 0.001mg/ℓ or less, which is less than the detectable level. On the other hand, the water to be treated was sent to the gas-liquid contact/adsorption unit 9 by a pump 17b. As shown in Fig. 9, air is supplied by a pump 19 from the bottom of the air exposing tank 18 to cause the water to be exposed to air in order to cause volatile contents of the water to be brought into air bubbles, and then the air bubbles are adsorbed on an activated carbon 20 above the water surface. 1,1,1-trichloroethane changed from liquid phase to gas phase was adsorbed by the activated carbon. Fig. 8 shows the results of decomposing experiments regarding the Test Water 2 containing trichloroethylene at 0.005ml per liter in the water to be treated, and the Test Water 1 simultaneously containing trichloroethylene at 0.05mg/ℓ and 1,1,1-trichloroethane at 8mg/ℓ. The experiments were carried out for both the case where hydrogen peroxide was added to only the tank 1 and the case where it was added to the tank 1 and just before the decomposing unit 7. In Fig. 8, (19) and (20) thereof show the results of the Test Water 2 containing only trichloroethylene at 0.05mg/ℓ, and (19) shows the results where hydrogen peroxide was added to only the tank 1, and (20) shows the results where hydrogen peroxide was added to the tank 1 and just before the decomposing unit 7. (21) and (22) thereof show the results of the Test Water 1 simultaneously containing both trichloroethylene of 0.05mg/ℓ and 1,1,1-trichloroethane of 8mg/ℓ. (21) shows the results when hydrogen peroxide was added to only the tank 1, and (22) shows the results when hydrogen peroxide was added to the tank 1 and just before the decomposing unit 7. As in Fig. 2, it is understandable that it is more effective to separately add hydrogen peroxide than to add it to only the tank even though the concentration of trichloroethylene is changed. The above preferred embodiments were based on the cases where the initial concentration of trichloroethylene is 8mg/ℓ and 0.05mg/ℓ with the concentration of trichloroethane fixed at 8mg/ℓ. However, even in cases where the initial concentration of trichloroethylene is more than 8mg/ℓ or less than 0.05mg/ℓ and the concentration of 1,1,1-trchloroethane is a value other than 8mg/ℓ, it was found that it is remarkably more effective to add hydrogen peroxide separately at two or more times than to add it once at the beginning. Furthermore, experiments which are similar to those carried out in the cases of trichloroethylene and 1,1,1-trichloroethane were carried out for water containing organic compounds, such as organic chlorine compounds, tetrachloroethylene, dichloroethylene, and dichloroethane in addition to trichloroethylene and 1,1,1-trichloroethane, and furthermore chloroform, bromodichloromethane, dibromochloromethane, bromoform, etc as various kinds of trihalomethane. Namely, according to the results for concentrations of 1 to 100mg/ℓ, in either case, although they can be decomposed with ultraviolet rays by adding hydrogen peroxide, the concentration was reduced to 0.001mg/ℓ by using the gas-liquid contact/adsorption treatment. In Fig. 1, it was more effective to add hydrogen peroxide to both the tank 1 and just before the decomposing unit 7 than to add it to only the tank 1. In a case where substances which need a much greater quantity of ultraviolet rays irradiation for decomposition such as chloroform, bromodichloromethane, etc are contained, the concentration was reduced to 0.001mg/ℓ in the water by treating them with the gas-liquid contact/adsorption unit 9 after having passed through the decomposing unit 7. Next, the water to be treated, which passed through the gas-liquid contact/adsorption unit 9, was fed to a tank 10 for the residual oxidizing agent removing unit, wherein a pump 14 is operated to supply sodium bisulfide stored in a storage tank 13 to the tank 10 in order to mix with the water to be treated. Thus, the oxidizing agent residual in the water was reduced and then discharged. In the above, the preferred embodiment copes with a situation wherein the oxidizing agents are removed through reduction by using sodium bisulfide in the tank 13. Activated carbon and/or resin may be alternately used for the same purpose. From the standpoint of handling, activated carbon is more advantageous. Furthermore, sodium hydroxide in a tank 15 and supplied by a pump 16 is also used for adjusting pH in line with the decomposition of the organic compounds. Furthermore, Fig. 1 shows a case where a single stage decomposing tank 7 is used for decomposing treatment. However, a decomposing unit of two or more tanks 7 may be connected and installed in series as shown in Fig. 10, and improved treatment may be carried out via the decomposing tanks 7 arranged one after another, or individual decomposing treatment may be carried out with a decomposing unit comprising tanks 7 installed parallel to each other as shown in Fig. 11. Furthermore, it is a matter of course that a decomposing unit of more than two tanks may be connected in series or parallel to each other to allow better decomposing treatment. In either case, it is more advantageous to add the oxidizing agent into piping just before the decomposing unit 7 by the pump 17a in addition to adding the oxidizing agent to the tank 1 by the pump 12.

Claims: A method of treating waste water containing organic compounds, comprising: adding a first amount of an oxidizing agent into said waste water to disinfect bacteria contained in said waste water, said first amount being suitable to substantially disinfect the bacteria contained in the waste water; removing solid material contained in said waste water treated with said oxidizing agent; adding a second amount of said oxidizing agent into said treated waste water, said second amount being selected such that the second amount and a part of the first amount remaining in the waste water are suitable to form hydroxy radicals for sufficiently decomposing the organic compounds in the waste water when ultraviolet rays are irradiated; irradiating the ultraviolet rays onto said treated waste water containing said oxidizing agent to form the active hydroxy radicals so that the organic compounds are decomposed by the hydroxy radicals formed by the part of the first amount and the second amount of the oxidizing agent; and removing said oxidizing agents remaining in said treated waste water. A method as claimed in claim 1, characterized by further comprising adjusting pH of the waste water while or after irradiating ultraviolet rays so that the waste water is processed. A method as claimed in any of claim 1 or 2, characterized in that said oxidizing agents are removed by at least one of reducing agent, activated carbon and catalyst. A method as claimed in claims 1 to 3, characterized in that the organic compounds are organic chlorine compounds. A method as claimed in any of claims 1 to 4, characterized in that said oxidizing agent is hydrogen peroxide or ozone. A method as claimed in claim 5, characterized in that said organic compounds include 1,1,1-trichloroethane. A method as claimed in any of claims 1 to 6, characterized by comprising the further step of exposing forcibly the waste water to air so that volatile organic materials contained in the waste water are retained in the air to adsorb onto activated carbon, subsequent to said decomposition step by irradiating with ultraviolet rays. A system for treating waste water containing organic compounds, comprising: a disinfection unit (1) for disinfecting bacteria contained in the waste water; a suspended solid removing device for separating solid substance contained in the waste water treated by the disinfection unit; a decomposition unit (7) having an ultraviolet ray lamp therein, said decomposition unit decomposing by the ultraviolet ray lamp the organic compounds contained in the waste water after suspended solid is removed; an oxidizing agent supplying unit (11) for supplying an oxidizing agent to the disinfection unit (1) and the decomposition unit (7), said oxidizing agent disinfecting the bacteria contained in the waste water when supplied at the disinfection unit and forming hydroxy radicals when irradiated by the ultraviolet rays to decompose the organic compounds at the decomposition unit; and an oxidizing agent removing unit (10) for eliminating the oxidizing agent remaining in the waste water treated at the decomposition unit, said oxidizing agent removing unit (10) including at least one of reducing agent, activated carbon and catalyst to remove the oxidizing agent in the waste water. A system for treating waste water as claimed in claim 8, characterized by further comprising a gas-liquid contact/adsorption unit (9) for forcibly exposing the waste water to air after the organic compounds are decomposed, volatile organic material contained in the waste water being retained in said air and being adsorbed onto activated carbon (20), wherein said gas-liquid contact/adsorption unit (9) includes an air-exposing tank (18) for receiving the waste water from the decomposition unit (7), air being fed into the waste water to catch the volatile organic materials in the air to separate from liquid, and an activated carbon layer (20) having activated carbon, said activated carbon layer absorbing the volatile organic material in the air.

Inventors: SEIJI TAKAYAMA, YOSHIHIRO KENMOKU, SEIJI, TAKAYAMA, YOSHIHIRO, KENMOKU, SEIJI, TAKAYAMA, C/O NEC ENVIRONMENT ENG. LTD., YOSHIHIRO, KENMOKU, C/O NEC ENVIRONMENT ENG. LTD.
Applicants: NEC ENVIRONMENT ENG LTD, NEC ENVIRONMENT ENGINEERING, LTD.
Application year: 1994
Main classification: C02F1
IPC codes: C02F1, B01D53, C02F9